CN202829892U - Sequential production equipment and system for polydextroses - Google Patents
Sequential production equipment and system for polydextroses Download PDFInfo
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- CN202829892U CN202829892U CN 201220407333 CN201220407333U CN202829892U CN 202829892 U CN202829892 U CN 202829892U CN 201220407333 CN201220407333 CN 201220407333 CN 201220407333 U CN201220407333 U CN 201220407333U CN 202829892 U CN202829892 U CN 202829892U
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- dextrose
- polydextroses
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Abstract
The utility model provides a sequential production equipment and system for polydextrose. The sequential production equipment and system for polydextroses comprises a reaction still, a cooling device, a vacuum unit, a smashing device, a membrane filtration refining plant, and a spray drying tower. The reaction still, the cooling device, the smash device, the membrane filtration refining plant, and the spray drying tower are in sequential connection. The equipment and system for polydextroses of the sequential production equipment and system for polydextroses can produce sugar-free polydextroses of high polymerization degree, higher stability, and high production.
Description
Technical field
The utility model relates to a kind of equipment of food food fibre, particularly a kind of continuous producing apparatus of poly-dextrose and system.
Background technology
Poly-dextrose (Polydextrose claims again ID) is a kind of of water-soluble dietary fibre, is white or off-white color powdery solid, odorless, soluble in water, be at citric acid, under the existence of sorbyl alcohol, glucose high-temperature low-pressure reactive polymeric is formed polymer, and its chemical formula is the polycondensate of the random bonding of glucose, but with 1, the 6-glycosidic link is combined into main D-Glucose polymer, be combined with a small amount of sorbyl alcohol, citric acid etc., molecular-weight average is greater than 3200, and mean polymerisation degree is greater than 20.Product form has A type, N-type, K type and modified polyglucose (Litesse) and refining poly-dextrose (II leqqeUltra) etc., the A type is amorphous powder, white is to faint yellow, and 10% pH value of water solution is 2.5～3.5, needs during application to regulate its acidity with buffer reagent; N-type is the aqueous solution of A type, and is colourless to faint yellow, concentration 70%, and the pH value is neutralized to 5.0～6.0 with KOH; The K type is to use food grade KHCO
3Regulate poly-dextrose pH value of water solution to 5.0～6.0, solution is concentrated, drying makes again, or with KOH, KHCO
3Be dry mixed with A type powder and form; Poly-dextrose is carried out catalytic hydrogenation processing obtain white to milky modified polyglucose, the pH value of 10% aqueous solution is 3.0～4.5, acidity and bitter taste reduce, taste has larger improvement, refining the refining poly-dextrose that forms on this basis is white solid, taste is salubrious, and the pH value of 10% solution is 4.5～6.5, the solution colorless and odorless.
Poly-dextrose has whole intestines, regulates the effect of blood sugar and blood fat, can be used as foodstuff fibre widespread use in various functional foodstuffs.In addition, also have following features:
The soluble dietary fibre poly-dextrose is a kind of polymer saccharide compound, belongs to the food fibre category, has whole intestines, regulates the effect of blood sugar and blood fat, can be used as foodstuff fibre widespread use in various functional foodstuffs.
1. low in calories, without carious tooth
Poly-dextrose is a kind of material low in calories (4.148kJ/g), is about 1/4th of general carbohydrate (16.5kJ/g); Without carious tooth, difficult digested.
2. good water holding and water-retaining capacity
Poly-dextrose has good moisture retention, and its water activity is lower, can prevent or delay the variation of water content in the food, helps to control increase or the loss speed of moisture in the food, by keeping moisture or preventing that water migration from prolonging the shelf-lives of product.
3. suitable viscosity
The viscosity of poly-dextrose solution is higher than the viscosity with isoconcentration sucrose or Sorbitol Solution USP. when the carbohydrate in replacing food and fat, can form desirable mouthfeel.
4. rectification freezing point
When using high-intensity sweetener to make frozen food confection low in calories, can add the matrix that poly-dextrose is adjusted product, compensation improves owing to freezing point reduces the bad texture change that causes because granulated sugar reduces the matrix forfeiture that causes.
5. good processing characteristics
The poly-dextrose stable in properties, good water solubility, the compatibility scope is wide, all can use in liquid and solid food, can be used in conjunction with numerous food supplementary materials.
The production system of poly-dextrose of the prior art, artificial link is more, is unfavorable for that quality control and productive rate are lower, in sum, a kind of low cost is provided, and the poly-dextrose production system that intelligent processing method, high yield and product stability are higher all is the hot issue of instantly social needs research.
The utility model content
For solving the problems of the technologies described above, the utility model provides a kind of continuous producing apparatus and system of poly-dextrose.
The utility model purpose provides a kind of continuous producing apparatus and system of poly-dextrose, comprise reactor, refrigerating unit, vacuum unit, shredding unit, membrane filtration refining plant and spray-drying tower, described reactor, refrigerating unit, shredding unit, membrane filtration refining plant and spray-drying tower are linked in sequence successively.
Preferably, described reactor is high temperature interlayer stainless steel cauldron.
Preferably, described refrigerating unit is single refrigerating unit or two refrigerating unit.
Preferably, said system also comprises discharge tank, and described discharge tank links to each other with described spray-drying tower.
More preferably, said system also comprises portioning machine, and described portioning machine links to each other with discharge tank.
The poly-dextrose continuous process system that the utility model provides is by the mechanical automation technology, and a plurality of links in the existing production method of improvement have been improved greatly quality control and production and productivity and realized automatic continuous production; By intellectuality control, can realize remote monitoring and the operation of whole system equipment; According to the requirement of actual production and equipment operation management, " four is distant " control of the remote signalling of feasible system, remote measurement, remote regulating, remote control.Improve output, and be beneficial to quality control and food security supervision.
Description of drawings
Continuous producing apparatus and the system schematic of the poly-dextrose that accompanying drawing 1 provides for the utility model.
Embodiment
Below in conjunction with specific embodiment, further illustrate the utility model.Should be understood that following embodiment only is used for explanation the utility model and is not used in the scope of the present utility model that limits.The experimental technique of unreceipted actual conditions in the following example, usually according to normal condition, or the condition of advising according to manufacturer.Ratio and per-cent are based on weight, unless stated otherwise.
Be the continuous producing apparatus of poly-dextrose of the present utility model and the rough schematic view of system such as Fig. 1, comprising: comprise reactor (1), refrigerating unit (2), vacuum unit (3), shredding unit (4), membrane filtration refining plant (5) and spray-drying tower (6), described reactor, refrigerating unit, shredding unit, membrane filtration refining plant and spray-drying tower are linked in sequence successively; In addition, said system also comprises heating unit (7), and described heating unit links to each other with described reactor; More preferably, said system also comprises portioning machine, and described portioning machine links to each other with spray-drying tower.
This system is when running, the material that mixes is at the reactor internal reaction, and reactor can adopt high temperature interlayer stainless steel cauldron, or the reactor of other similar purposes, keep temperature of reaction by the circulation of heating unit, by the vacuum tightness in the vacuum unit I maintenance reactor;
With the completely reacted poly-dextrose crude product access prior refrigerating unit crossed of cleaning and sterilization, opening power, then open the baiting valve of reactor bottom, the poly-dextrose crude product of gained just flows in the refrigerating unit, the product of gained is rapid grumeleuse and be sent to the flaker tail end therein, then is delivered to the temporary tank of material;
Before the pulverizing first the alcohol with 75% pulverizer stainless steel mesh and food contact surface are carried out spray disinfectant, install 80 order stainless steel meshs, open the pulverizer power supply, open again the motor under the temporary tank of material, the mass transport in the temporary tank of material is pulverized to pulverizer;
Adopting the activated carbon decolorizing device that product is decoloured makes 10% product solution to white or the off-white color and treats next step processing;
Dissolving or the liquid product solution after decolouring are circulated through membrane filtration, with the impurity of further reduction product, the liquid after concentrating flows into concentrated fluid cylinder, is specially: open membrane sepn head tank water intaking valve, begin simultaneously to stir, inject pure water to 200cm to head tank.Open the membrane sepn head tank and advance the film valve, start auxiliary pump, after stable, start main pump, progressively heighten the main pump frequency to 32H
ZAbout, the open degree of corresponding adjusting concentrated solution valve is come controlling diaphragm assembly intake pressure and flow simultaneously.Pressure-controlling is about 11.4MPa, and flow when being filled into the 100cm left and right sides, begins to add water to 200cm at 500LPM, and the main pump frequency of turning down during to the 70cm left and right sides to be filtered is down to 20 when frequency and is closed main pump when following, closes auxiliary pump.Control temperature of charge below 42 ℃ by regulating the interchanger cooling water flow.Penetrating fluid flows into the clear liquid tank by pipeline.Then open water pot, with pure water the feed liquid in the film is pushed back storage tank; To further be concentrated into concentration by the triple effect thickening equipment through the concentrated solution in the concentrated fluid cylinder of being stored in of membrane filtration is 40～70%, wherein under meter is controlled at 10～15LPM, makes product more be conducive to carry out vacuum-drying; Concentrated solution after will concentrating by triple effect makes product become the needed powdery in commercially available prod through vacuum dehydrating at lower temperature; Can obtain the Sugarless poly-glucose finished product.
Be necessary at last in this explanation to be: above embodiment only is used for the technical solution of the utility model is described in more detail; can not be interpreted as the restriction to the utility model protection domain, some nonessential improvement and adjustment that those skilled in the art makes according to foregoing of the present utility model all belong to protection domain of the present utility model.
Claims (3)
1. the continuous producing apparatus of a poly-dextrose and system, it is characterized in that: it comprises reactor, refrigerating unit, vacuum unit, shredding unit, membrane filtration refining plant and spray-drying tower, and described reactor, refrigerating unit, shredding unit, membrane filtration refining plant and spray-drying tower are linked in sequence successively.
2. the continuous producing apparatus of poly-dextrose as claimed in claim 1 and system, it is characterized in that: described reactor is high temperature interlayer stainless steel cauldron.
3. the continuous producing apparatus of poly-dextrose as claimed in claim 1 and system, it is characterized in that: it also comprises portioning machine, described portioning machine links to each other with described spray-drying tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220407333 CN202829892U (en) | 2012-08-16 | 2012-08-16 | Sequential production equipment and system for polydextroses |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220407333 CN202829892U (en) | 2012-08-16 | 2012-08-16 | Sequential production equipment and system for polydextroses |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202829892U true CN202829892U (en) | 2013-03-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220407333 Expired - Fee Related CN202829892U (en) | 2012-08-16 | 2012-08-16 | Sequential production equipment and system for polydextroses |
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| Country | Link |
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| CN (1) | CN202829892U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104277140A (en) * | 2013-07-04 | 2015-01-14 | 河南泰利杰生物科技有限公司 | Continuous cooling production technology of polydextrose liquid, and production apparatus thereof |
-
2012
- 2012-08-16 CN CN 201220407333 patent/CN202829892U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104277140A (en) * | 2013-07-04 | 2015-01-14 | 河南泰利杰生物科技有限公司 | Continuous cooling production technology of polydextrose liquid, and production apparatus thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Free format text: FORMER OWNER: WINWAY BIOTECHNOLOGY NANTONG CO., LTD. Effective date: 20150504 Owner name: TAILAI FOOD INGREDIENT (NANTONG) CO., LTD. Free format text: FORMER OWNER: SHANGHAI BOCHENG BIOTECHNOLOGY CO., LTD. Effective date: 20150504 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 201317 PUDONG NEW AREA, SHANGHAI TO: 226400 NANTONG, JIANGSU PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20150504 Address after: 226400 hi tech Industrial Development Zone, Nantong County, Jiangsu, Rudong Patentee after: Taylor food ingredients (Nantong) Co. Ltd. Address before: 201317 Shanghai hangtou town Pudong New Area Bridge Road No. 2 Building 5 Patentee before: Shanghai Winway Biotechnology Co., Ltd. Patentee before: BOCHENG BIOTECHNOLOGY NANTONG CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130327 Termination date: 20180816 |